High-softening-point asphalt as well as preparation method and application thereof
A technology of high softening point asphalt and softening point, which is applied in the direction of carbon preparation/purification, chemical processing of tar pitch/petroleum pitch/natural pitch, solidification/crushing processing of tar pitch/petroleum pitch/natural pitch, etc., which can solve Problems such as high foaming pressure, popularization or practical application, to achieve the effect of reducing the cost of preparation
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Embodiment 1
[0028] Put 200g of medium-temperature coal tar pitch in a magnetically stirred reactor, and raise the temperature to 280°C at a heating rate of 5°C / min. During the stirring process, air was introduced, wherein the air flow rate, stirring speed and stirring time were 200mL / min, 200rpm, and 2h, respectively. The softening point of the prepared high softening point pitch is 245°C, the content of n-heptane solubles (HS) is 8.9%, the content of toluene solubles (TS) is 18.3%, the content of toluene insoluble-pyridine solubles (TI-PS ) content was 13.6%, pyridine-insoluble-quinoline-soluble (PI-QS) content was 11.1%, and quinoline-insoluble (QI) content was 57%. 10g of the high softening point asphalt was crushed to 10μm, then placed in a tubular reactor and sealed, first raised to 300°C at a heating rate of 5°C / min and kept at a constant temperature for 2 hours, then raised to 300°C at a heating rate of 10°C / min 600°C and constant temperature for 1h to obtain unfoamed bulk carbon....
Embodiment 2
[0030] The high softening point asphalt prepared in Example 1 was vacuumized at 300°C / 80kPa for 1.5h, and the light components extracted accounted for 8% of the total mass of the high softening point asphalt. Example 1 After the high softening point asphalt is vacuumized, its softening point is 252°C, the content of n-heptane solubles (HS) is 1.2%, the content of toluene solubles (TS) is 12.5%, and the content of toluene insoluble- The pyridine soluble (TI-PS) content was 9.4%, the pyridine insoluble-quinoline soluble (PI-QS) content was 9.9%, and the quinoline insoluble (QI) content was 67%. 10g of the high softening point asphalt was crushed to 10μm, then placed in a tubular reactor and sealed, first raised to 300°C at a heating rate of 5°C / min and kept at a constant temperature for 2 hours, then raised to 300°C at a heating rate of 10°C / min 600°C and constant temperature for 1 hour to obtain foamed carbon with uniform pore size, wherein the average pore size of the foamed c...
Embodiment 3
[0032] The high softening point asphalt prepared in Example 1 was vacuumized at 320°C / 80kPa for 1.5 hours, and the light components extracted accounted for 13% of the total mass of the high softening point asphalt. Example 1 After the high softening point asphalt is vacuumized, its softening point is 257°C, the content of n-heptane solubles (HS) is 0%, the content of toluene solubles (TS) is 10.2%, and the content of toluene insoluble- The pyridine soluble (TI-PS) content was 10.8%, the pyridine insoluble-quinoline soluble (PI-QS) content was 10.2%, and the quinoline insoluble (QI) content was 68.8%. 10g of the high softening point asphalt was crushed to 10μm, then placed in a tubular reactor and sealed, first raised to 300°C at a heating rate of 5°C / min and kept at a constant temperature for 2 hours, then raised to 300°C at a heating rate of 10°C / min 600°C and constant temperature for 1 hour to obtain foamed carbon with uniform pore size, wherein the average pore size of the ...
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